AU762213B2 - Method and apparatus for shaping particles by ultrasonic cavitation - Google Patents

Abstract

Method of shaping solid, particulate materials, which comprises forming a raw slurry of the starting material, in a liquid which is a partial solvent of said material, and submitting the slurry to treatment by ultrasound generators to produce therein ultrasonic vibrations which shape and grind the starting, particulate material to produce a shaped slurry of ground and shaped particles. The shaped particles may be separated from their slurry by removing the partial solvent by decantation and/or filtration. The partial solvent may be a liquid in which the material to be shaped has a solubility comprised between 1 and 10, wherein the solubility is expressed as grams of material that are dissolved in 100 ml of the liquid at a temperature of 20° C. The partial solvent can be chosen from among acetone, methyl ethyl ketone, and mixtures of said solvents with one another or other solvents and/or a minor amount of water, and may also be an organic solvent.

Description

WO 00/41984 PCT/ILOO/00003 -1- METHOD AND APPARATUS FOR SHAPING PARTICLES BY ULTRASONIC CAVITATION Field of the Invention This invention relates to method and apparatus for the ultrasonic shaping of particles, particularly of organic compounds, which permit to obtain by ultrasonic cavitation shaped particles having smooth and rounded surfaces. The method and apparatus can produce shaped particles of different sizes and can also grind the particles. Typical, but not exclusive, applications of the invention are the shaping of high explosives, solid propellants, and pharmaceuticals.

Background of the Invention The use of ultrasonic cavitation has been proposed in the microbiological and pharmaceutical field: thus McIntosh, A. F. and R.F. Munro, in "Ultrasonic Treatment of Microorganism", Process Biochem 6 22-3, 37 (1971) and Gold in "Ultrasonic Sterilization of Pharmaceutical Preparations", 1962, Thesis, University of Connecticut Storrs, CT, USA 06268. Ultrasonic cavitation can produce the mechanical disruption of cell membranes.

Ultrasonic cavitation can also be used for grinding solid particulate materials, including even explosives and solid propellants. The state of the art in this respect is summarized in USP 5,035,363, the content of which is herein included by reference.

One of the known processes for grinding explosives and solid propellants is wet grinding, viz. grinding of a slurry of a solid material in a liquid; and a particular form of wet grinding is ultrasonic grinding, in which a slurry of a solid material in a liquid is subjected to ultrasonic vibrations.

WO 00/41984 PCT/IL00/00003 -2- USP 5,035,363 discloses an ultrasonic grinding process, which includes suspending the particles to be ground in a liquid to form a slurry and subjectingthe slurry to ultrasonic energy at a frequency or frequencies in the range of about 14 to 60 KHz.

The liquid medium of the slurry must be inert, viz. not reactive chemically with the explosive material being ground, and must also be a non-solvent as regards said material. The preferred slurry liquid is water or other aqueous liquid medium. The explosives mentioned in said application are cyclotrimethylenetrinitramine

(RDX),

tetramethylenetetranitramine (HMX) and a mixture of RDX and HMX known as co-produced explosive (CPX).

The apparatus disclosed in said patent comprises an ultrasound generator, including a transducer and a sonic converter, which imparts ultrasonic vibrations to the tip of a disruptor horn. A vessel is provided, into which flows an input stream of a slurry containing the unground explosive particles and out of which flows an output stream of the slurry containing the ground explosive particles. The tip of the disruptor horn is submerged in the slurry and is located so that all particles passing through the apparatus are subjected to a high intensity ultrasonic field below the tip, where the primary acoustic cavitation occurs, the stream of ground particles flowing through an orifice located immediately below the tip of the horn and therefrom to the apparatus outlet. In said patent, however, no consideration is given to the shape of the ground particles and rounded particles are not obtained.

An attempt to improve the crystal shape and surface smoothness of particles of RDX, without changing their size, is described by A. van der Steen et al, in "Crystal Quality and Less Sensitive Explosives", a paper presented at the "Insensitive Munitions Technology Symposium", 16-18 June 1992, Williamsburg, VA, USA. The Authors treated spheroidized RDX particles with saturated acetone and then with unsaturated P:\OPERU\Jcc\ 18877-00 sp.doc- 18/03103 -3acetone or ethyl acetate. Smoother surfaces and flattened crystal shapes were thus obtained.

Experience has shown that the shape of the particles is of the highest importance, and more precisely, it is highly desirable that the ground particles have smooth surfaces and a generally rounded shape, approaching a spherical shape. A rounded shape improves the flowability of the particles when they are used in composite paste materials. It permits better packaging, increasing the amount of material that can be packaged in a given space, e.g. providing more solid loading of powder in explosives, solid propellants and other particulate material.

The present invention seeks to provide a shaping method and apparatus that permits shaping of solid, particulate materials, preferably of organic compounds, in such a way as to obtain particles that have smooth and rounded surfaces and that approach spherical shape.

The present invention also seeks to provide a shaping method and apparatus that are I o particularly suited for shaping high explosives, solid propellants, or solid pharmaceutical *.o preparations.

The present invention yet further seeks to provide: a shaping method and apparatus which are capable of producing powders of improved flowability and packaging properties; a shaping method that is efficient and of limited cost; and a shaping method that does not produce an uncontrolled reduction of the size of the particles.

P:'OPERUcc\ 18877-00 sp-t.do- 18/03/03 -4- The present invention further seeks to provide a method and apparatus which, when applied to the shaping of explosives, are secure and do not generate temperatures which exceed a safe limit.

The present invention seeks to achieve the aforesaid purposes by a method and apparatus which are simple and inexpensive.

Accordingly, the present invention provides a method of shaping a solid, particulate material by application of ultrasonic vibration which method comprises suspending said solid, particulate material in a liquid which is a partial solvent for said solid, particulate material to form a starting suspension, and applying ultrasonic vibration to said suspension thereby shaping the grinding said solid, particulate material to produce a final suspension of ground and rounded particles.

The shaping method of the invention comprises forming a raw slurry, viz. a slurry of the starting, particulate material, in a liquid which is a partial solvent of said material, and submitting the slurry to treatment by ultrasound generators to produce therein ultrasonic vibrations which shape the starting, particulate material to produce a shaped slurry. "Shaped slurry" means herein a slurry of shaped, viz. rounded, near spherical, ground particles.

It is known that the generation of a high frequency, ultrasonic vibration field in liquids results in cavitation and in the production of high local pressures. The high pressure in the cavities, near the particles suspended in the partial solvent, normally produces a grinding effect, sharply reducing the particles size, as is taught in the prior art. Surprisingly it has been found that in the process and apparatus of this invention ultrasonic vibrations in the appropriate liquid produce a shaping effect, imparting to the particles a rounded, near spherical configuration. The shaping is accompanied by a grinding effect, viz. a reduction of the particles size. Whether the shaping or the grinding effect is predominant, depends on the frequency of the vibrations, on the energy density, on the type of the liquid and on the properties of the material, viz.

whether it is easy or hard to grind. Higher frequencies increase the shaping effect.

While the frequencies used in the method according to the invention are preferably from 20 KHz to 50 KHz, shaping is generally predominant at frequencies above KHz, and grinding is generally predominant at frequencies below 25 KHz. Between KHz and 40 KHz, both effects are present in varying ratios.

The shaped particles can be separated from their slurry by removing the partial solvent, by means appropriate to the particular partial solvent and to the material of the particles, which can include decantation and/or filtration.

By "partial solvent" is meant a liquid, typically water or a liquid comprising or consisting of an organic compound, in which the material to be ground-shaped has a solubility comprised between 1 and 10, wherein the solubility is expressed as grams of material that are dissolved in 100 ml of the liquid at a temperature of 209C.

Examples of such partial solvents are organic solvents such as acetone, methyl ethyl ketone, and mixtures of said solvents with one another or other solvents and/or a minor (such as less than 10wt%) amount of water.

Preferably, the partial solvent used should have a boiling point from 40* to 100 0

C.

It is generally preferred to stir the slurries both the raw and the shaped slurry during the shaping operation. Preferably, the stirring speed should be from 100 to 800 rpm. Also preferably the ultrasound energy density should be from 10 to watts/liter.

The method of the invention is generally applicable to the shaping of solid, particulate materials of organic compounds, but preferred embodiments thereof are the shaping PAOPERJcc\IS8877-0 spcc-2.dc-16/04/03 -6of high explosives, solid propellants and pharmaceutical compounds or compositions, and high cost organic materials. Optionally, and particularly if explosives or solid propellants are ground, the method further comprises cooling the slurry during the shaping, to avoid a temperature rise above a safe limit, which depends upon the particular explosive or solid propellant being treated.

The method of the invention can be carried out in batch, semi-batch or continuous operation.

The raw slurry should contain an amount of solid, particulate material from 10 wt% to wt%. The dimensions of the raw particles of the material to be shaped should not exceed 2000 m.

The invention also provides an apparatus suitable for carrying out the method of the invention as described herein. The apparatus comprises a vessel defining a treatment space, having an inlet for the starting suspension and an outlet for the final suspension, and ultrasound generators for producing ultrasonic vibrations in said treatment space, characterized in that the ultrasound generators are located at the periphery of the treatment space.

2 The apparatus according to the invention thus comprises a vessel defining a treatment space, having an inlet for the raw slurry and an outlet for the shaped slurry, and generators of ultrasonic vibrations that are distributed about the periphery of the treatment space, viz.

the space occupied by the slurry which is being transformed from raw to shaped, in order to obtain an efficient ultrasonic cavitation field. Stirring means are provided and assure that the particles of the slurry, as it is so transformed, are uniformly exposed to the "•ultrasound and a homogeneous product is obtained. The apparatus of the invention may S be adapted to carry out the method of the invention in batchwise manner. In any case, the volume of the treatment space, and therefore of the slurry which is subjected to ultrasonic 30 vibrations, is related to the power applied in such a way as to obtain the energy densities hereinbefore specified.

P:'OPERcc\18877-00 spc.doc.- I03/03 -7- The apparatus preferably comprises stirring means for assuring the homogeneity of the slurry; and cooling means, particularly when the material to be shaped is an explosive or a solid propellant.

The frequency of the ultrasonic vibrations is preferably from 20 to 50 KHz. The power applied through the ultrasonic vibrations is preferably 10 to 50 watts/liter.

The method and apparatus of the invention are not limited to the shaping of any particular solid, particulate material, since and operative parameters of the method and the structure of the apparatus can be adjusted by the skilled person, depending on the nature of the material.

Brief Description' of the Drawings Embodiments of the present invention are illustrated in the accompanying non-limiting drawings in which: Fig. 1 is a plane view from above of a vessel, which is the part of the 20 apparatus in which.the ultrasonic shaping occurs, according to an embodiment of the invention; Fig. 2 is an axial cross-section of the vessel of Fig. 1; Fig. 3 is a schematic view of the vessel of Figs. 1 and 2, mounted on a movable container for receiving the shaped slurry; 25 Fig. 4 is a perspective view from above of the vessel of Figs. 1 and 2, in which the ultrasonic generators have been introduced; Figs. 5 and 6 are photographs of RDX and HMX particles, respectively, not treated according to the invention; and Figs. 7 and 8 are photographs of RDX and HMX particles, respectively, treated according to the invention.

In the following description, reference is made particularly to explosives, typical examples of which are RDX, HMX and CPX, but this is done only for illustrative purposes, and is not to be construed as a limitation of the invention to the shaping of explosives.

With reference now to Figs. 1 and 2, numeral 10 generally designates a cavitation vessel in which the cavitation and the shaping of the slurry occurs and the inside of which constitutes the treatment space; Cavitation vessel 10 is provided with double wall 11, made e.g. of metal sheets, forming a space through which a cooling fluid is introduced through an inlet 12 and discharged through an outlet 13. The cavitation vessel also has a bottom 14, which is slanted to facilitate discharge of the slurry of shaped particles from the latter, and in the center of which a shaped slurry outlet 15 is provided. Numeral 16 designates posts which occupy spaces that are not in the effective zone for the cavitation process, so that. if they were filled with liquid, this would not take part in said process. Numeral 20 indicates the ultrasonic .generators i"0" that will be described later on. The vessel 10 is also provided with a preferably double-walled cover 17 that is visible only in Fig. 3, and which is provided with any suitable attachments for connecting it to vessel 10. Cover 17 supports a motor 18, which actuates a stirrer, not illustrated in the drawings, through an opening for its shaft.

As seen in Fig. 4, ultrasound generators, or more precisely, the transducers that generate the ultrasound, designated by numeral 20, are mounted by means of hooks 21 on the cavitation vessel 10, so that they almost completely surround the treatment space in which the ultrasonic shaping occurs. The ultrasound generators may be of any type, such as known in the art. The ultrasonic vibrations gradually transform the raw slurry to a shaped slurry.

The cavitation vessel 10 may be conveniently mounted on a receptor container into Which the slurry of the ground particles is emptied after the shaping has been terminated. The receptor container 25 can be mounted, if desired, on wheels 26, to make it mobile.

Figs. 5 to 8 are photographs of RDX and HMvO particles illustrating the shaping effect of an embodiment of the invention. A comparison of Fig. 5 with Fig. 7 and of Fig. 6 with Fig. 8 shows. that. the treatment of the invention has produced mostly well rounded particles from raw particles that had shapes from very angular to sub-angular.

The following are non-limitative examples illustrate embodiments of the present invention.

Example 1 Production of rounded HMvX particles in the size of 60 umr 1500 gr of fine HMX are suspended in 3000 ml of technical acetone and are stirred for 4 hours, while subjecting the suspension to ultrasound vibration having a frequency of 40 K.Hz. The stirring speed is 180 rpm and the energy density of the ultrasound is 50 watts/liter.

Ex~e 2 Production of rounded RDX in the size of 150 tirn gr of coarse RDX are suspended in 100 ml ethanol and stirred for 1.5 hours, whie subjecting the suspension to ultrasound vibration having a frequency of 25 KHz. The **stirring speed is 15 0 rpm and the energy density of the ultrasound is 10 watts/liter.

P:OPERU\cc\8877-00 spccdoc-18/03/03 While embodiments of the invention have been described by way of illustration, it will be understood that the invention can be carried out with many modifications, variations and adaptations, without departing from its spirit or exceeding the scope of the claims.

Throughout this specification and the claims which follow, unless the context requires otherwise, the word "comprise", and variations such as "comprises" and "comprising", will be understood to imply the inclusion of a stated integer or step or group of integers or steps but not the exclusion of any other integer or step or group of integers or steps.

The reference to any prior art in this specification is not, and should not be taken as, an acknowledgment or any form of suggestion that that prior art forms part of the common general knowledge in Australia.

*Oda a •go 6 4J

Claims (14)

1. A method of shaping a solid, particulate material by application of ultrasonic vibration which method comprises adding said solid, particulate material to a liquid which is a partial solvent for said solid, particulate material to form a starting suspension, and applying ultrasonic vibration to said suspension thereby shaping the grinding said solid, particulate material to produce a final suspension of ground and rounded particles.

2. A method according to claim 1, further comprising separating the ground and shaped particles from the final suspension by removing the liquid.

3. A method according to claim 2, wherein the liquid is removed by decantation and/or filtration.

4. A method to any one of the preceding claims, wherein the liquid in which the material to be shaped has a solubility between 1 and 10, expressed as grams of material that are dissolved in 100 ml of the liquid at a temperature of 20 0 C. oooo 2 5. A method according to any one of the preceding claims, wherein the liquid is an organic solvent.

6. A method according to claim 5, wherein the organic solvent is chosen from acetone, methyl ethyl ketone, and mixtures of said solvents with one another or other solvents and/or a minor amount of water.

7. A method according to claim 5, wherein the liquid has a boiling point from 400 to 100C.

8. Method according to any one of the preceding claims, further comprising stirring the starting suspension during the application of ultrasonic vibration. P:\OPERcc\Ji8877-O0 sp.doc-18/03/03

12- 9. A method according to any one of the preceding claims, wherein the solid, particulate material is a high explosive or solid propellant. A method according to any one of claims 1 to 8, material is a pharmaceutical compound or composition. 11. A method according to any one of claims 1 to 8, material is a high cost organic material. 12. A method according to claim 9, further comprising the application of ultrasonic vibration. wherein the solid, particulate wherein the solid, particulate cooling the suspension during

13. Method according to any one of the preceding claims, wherein the starting suspension contains from 10 wt% to 75 wt% of solid, particulate material.

14. A method according to any one of the preceding claims, wherein the dimensions of the particles of solid, particulate material do not exceed 2000 gm. A method according to any one of the preceding claims, wherein the ultrasonic vibration is applied at a frequency of from 20 to 50 KHz.

16. A method according to any one of the preceding claims, wherein the ultrasonic vibration has an ultrasound energy density of from 10 to 50 watts/liter. 25 17. An apparatus suitable for shaping solid, particulate material in accordance with the method claimed in claim 1, which apparatus comprises a vessel defining a treatment space, having an inlet for the starting suspension and an outlet for the final suspension, and ultrasound generators for producing ultrasonic vibrations in said treatment space, characterized in that the ultrasound generators are located at the periphery of the treatment space. P:\OPER\Jcc\18877-00 spcc.doc-i/03/03 13-

18. An apparatus according to claim 17, further comprising stirring means for assuring homogeneity of the suspension and their uniform exposure to the ultrasound.

19. An apparatus according to claim 17 or 18, further comprising cooling means. A method according to claim 1 substantially as hereinbefore described with reference to the Examples.

21. An apparatus according to claim 17 substantially as hereinbefore described with reference to Figures 1 to 4. Dated this 20 th day of March 2003 Rafael-Armament Development Authority Ltd. by DAVIES COLLISON CAVE Patent Attorneys for the Applicant(s) S S. 0 .0